[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

EP0061346A2 - Dispersant composition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture - Google Patents

Dispersant composition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture Download PDF

Info

Publication number
EP0061346A2
EP0061346A2 EP82301504A EP82301504A EP0061346A2 EP 0061346 A2 EP0061346 A2 EP 0061346A2 EP 82301504 A EP82301504 A EP 82301504A EP 82301504 A EP82301504 A EP 82301504A EP 0061346 A2 EP0061346 A2 EP 0061346A2
Authority
EP
European Patent Office
Prior art keywords
composition
dispersant
amine
group
lubricating oil
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP82301504A
Other languages
German (de)
French (fr)
Other versions
EP0061346A3 (en
EP0061346B1 (en
Inventor
Robert Edward Malec
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Edwin Cooper Inc
Original Assignee
Edwin Cooper Inc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Edwin Cooper Inc filed Critical Edwin Cooper Inc
Publication of EP0061346A2 publication Critical patent/EP0061346A2/en
Publication of EP0061346A3 publication Critical patent/EP0061346A3/en
Application granted granted Critical
Publication of EP0061346B1 publication Critical patent/EP0061346B1/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M163/00Lubricating compositions characterised by the additive being a mixture of a compound of unknown or incompletely defined constitution and a non-macromolecular compound, each of these compounds being essential
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/06Well-defined aromatic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/02Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers
    • C10M2205/028Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing acyclic monomers containing aliphatic monomers having more than four carbon atoms
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2205/00Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions
    • C10M2205/06Organic macromolecular hydrocarbon compounds or fractions, whether or not modified by oxidation as ingredients in lubricant compositions containing conjugated dienes
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/281Esters of (cyclo)aliphatic monocarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/282Esters of (cyclo)aliphatic oolycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/283Esters of polyhydroxy compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/286Esters of polymerised unsaturated acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2207/00Organic non-macromolecular hydrocarbon compounds containing hydrogen, carbon and oxygen as ingredients in lubricant compositions
    • C10M2207/28Esters
    • C10M2207/34Esters having a hydrocarbon substituent of thirty or more carbon atoms, e.g. substituted succinic acid derivatives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2209/00Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
    • C10M2209/02Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C10M2209/08Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
    • C10M2209/084Acrylate; Methacrylate
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/02Amines, e.g. polyalkylene polyamines; Quaternary amines
    • C10M2215/04Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms
    • C10M2215/042Amines, e.g. polyalkylene polyamines; Quaternary amines having amino groups bound to acyclic or cycloaliphatic carbon atoms containing hydroxy groups; Alkoxylated derivatives thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/22Heterocyclic nitrogen compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/22Heterocyclic nitrogen compounds
    • C10M2215/221Six-membered rings containing nitrogen and carbon only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/22Heterocyclic nitrogen compounds
    • C10M2215/225Heterocyclic nitrogen compounds the rings containing both nitrogen and oxygen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/22Heterocyclic nitrogen compounds
    • C10M2215/225Heterocyclic nitrogen compounds the rings containing both nitrogen and oxygen
    • C10M2215/226Morpholines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2215/00Organic non-macromolecular compounds containing nitrogen as ingredients in lubricant compositions
    • C10M2215/30Heterocyclic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/044Sulfonic acids, Derivatives thereof, e.g. neutral salts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2219/00Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
    • C10M2219/04Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions containing sulfur-to-oxygen bonds, i.e. sulfones, sulfoxides
    • C10M2219/046Overbasedsulfonic acid salts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2223/00Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2223/02Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
    • C10M2223/04Phosphate esters
    • C10M2223/045Metal containing thio derivatives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2225/00Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions
    • C10M2225/04Organic macromolecular compounds containing phosphorus as ingredients in lubricant compositions obtained by phosphorisation of macromolecualr compounds not containing phosphorus in the monomers
    • C10M2225/041Hydrocarbon polymers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2227/00Organic non-macromolecular compounds containing atoms of elements not provided for in groups C10M2203/00, C10M2207/00, C10M2211/00, C10M2215/00, C10M2219/00 or C10M2223/00 as ingredients in lubricant compositions
    • C10M2227/06Organic compounds derived from inorganic acids or metal salts
    • C10M2227/061Esters derived from boron
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2010/00Metal present as such or in compounds
    • C10N2010/04Groups 2 or 12
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • C10N2040/251Alcohol-fuelled engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • C10N2040/255Gasoline engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/25Internal-combustion engines
    • C10N2040/255Gasoline engines
    • C10N2040/28Rotary engines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2070/00Specific manufacturing methods for lubricant compositions
    • C10N2070/02Concentrating of additives

Definitions

  • This invention relates to a dispersant canposition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture.
  • Dispersants are used in engine lubricating oil to prevent sludge formation and to inhibit varnish on hot engine surfaces such as pistons.
  • Hydrocarbon-substituted succinimides are quite effective in such use (U.S. Patent 3,172,892).
  • succinimides of hydroxyalkyl substituted amines have been shown to be effective (U.S. Patent 3,219,666).
  • Boronation of such succinimides has also been practiced (U.S. Patents 3,322,670; 3,254,025 and 3,087,936). Boronation processes are also taught in U.S. Patents 3,082,955; 3,950,341 and 3,089,936.
  • Mannich dispersants made fran hydrocarbon-substituted phenols, formaldehyde and amines are also known (U.S. Patents 3,413,347; 3,725,277; 3,368,972 and 3,798,165).
  • Boron-modified Mannich dispersant are described in U.S. Patents 3,697,574; 3,703,536; 3,704,308; 3,751,365; and 3,756,953.
  • Fatty acid modified Mannich dispersants are described in U.S. Patents 3,798,247 and 3,803,039. Further representative U.S. patents include the following:- and in addition, reference can be made to British Patent 1,362,013
  • dispersant compositions which contain a synergistic mixture of (a) a boronated hydrocarbon-substituted succinic amide/imide/ester of an oxyalkylated anine and (b) a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and an anine, and, optionally, a boronating agent and/or fatty acid .
  • a synergistic mixture of (a) a boronated hydrocarbon-substituted succinic amide/imide/ester of an oxyalkylated anine and (b) a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and an anine, and, optionally, a boronating agent and/or fatty acid .
  • These compositions may be added to lubricating oil (or the ingredients thereof may be so-added separately).
  • ASIM Sequence VD engine test the synergistic canbination
  • a preferred embodiment of the invention is a lubricating oil composition
  • a lubricating oil composition comprising a major amount of an oil of lubricating viscosity containing a minor dispersant amount of a synergistic combination of dispersants, said combination comprising
  • the invention also provides a boronated hydrocarbon- substituted succinic amide/imide and/or ester of an oxyalkylated amine or a Mannich condensation product of a hydrocarbon-substituted phenol, fonnaldeyhyde and an amine, and, optionally a boronating agent and/or a fatty acid, in either case intended for use in a synergistic dispersant mixture comprising at least one representative of each of the aforesaid dispersants.
  • the boronated succinimide dispersant can be made by reacting an aliphatic hydrocarbon-substituted succinic acid anhydride or lower alkyl ester with an oxyalkylated amine and a boronating agent in the approximate mole ratio of 1.0:0.2-2, 0:001-5.0.
  • the preferred succinic reactant is an aliphatic hydrocarbon-substituted succinic anhydride in which the aliphatic hydrocarbon group has a molecular weight of 700-50, 000.
  • the aliphatic hydrocarbon group is preferably derived from an olefin polymer such as polypropylene, polybutene, ethylene-propylene copolymer, ethylene-propylene-1, 4-hexadiene copolymer ethylene-propylene-1,4-cyclohexadiene copolymer, ethylene-propylene-1,5-cycloctadiene copolymer, ethylene-propylene-5-methylene-2-norbomene, or etylene-propplene-2, 5-norbornadiene copolymer.
  • an olefin polymer such as polypropylene, polybutene, ethylene-propylene copolymer, ethylene-propylene-1, 4-hexadiene copolymer
  • the most preferred aliphatic hydrocarbon substituent is derived from an olefin polymer having a molecular weight of 700-5000. These include the olefin polymers mentioned above which have the more preferred molecular weight. Of the above, polybutene is most preferred.
  • a high molecular weight of olefin polymer for example, one having a molecular weight of 50, 000 or more can be degraded to produce an olefin polymer having a more preferred molecular weight.
  • Methods of reducing the carbon chain length of olefin polymers by shearing are well known. Mere heating with mechanical stirring will reduce molecular weight. Air can be injected into heated polymer to cause degradation and reduce molecular weight. Extrusion through an orifice under pressure causes chain scission. Any combination of such methods can be used.
  • Highly preferred olefin polymers for use in making the succinic substituent are polymers of butene. Of these, the most preferred are the polybutenes having an average molecular weight of 700-2000.
  • the hydrocarbon substituent can be introduced by heating a mixture containing the olefin polymer and maleic anhydride to 200-250°C.
  • the reaction can be catalyzed by injecting chlorine.
  • a peroxide catalyst can be used.
  • the reaction is preferably conducted in a mineral oil diluent which can remain in the succinic product to act as a.solvent in later stages of the preparation.
  • the aliphatic hydrocarbon-substituted succinic anhydrides are well known.
  • the oxyalkylated amines are readily made by reacting an alkylene oxide with an amine having primary and/or secondary amine groups.
  • the preferred alkylene oxides are ethylene oxide, propylene oxide, and butylene oxide. The more preferred are ethylene oxide, and propylene oxide or mixtures thereof.
  • the most preferred oxyalkylating agent is ethylene oxide.
  • the amines which are oxyalkylated are those containing 2 to 10 nitrogen atoms. More preferably, they also contain about 2-20 carbon atoms. Some examples of these amines are ethylenediamine, 1, 2-propylene- diamine, 1, 3-propanediamine, N-aminoethyl piperazine, N-oleylaminopropyl-1, 3-propane diamine, diethylene triamine, triethylene tetramine, tetraethylene pentamine, pentaethylene hexamine, N-dodecyl ethylenediamine, N-dodecyl- 1, 3-propane diamine, N-octadecyl diamine, N-(decylaminoethyl) ethylenediamine and the like.
  • the preferred amines for use in making the succinic dispersants are the polyalkyleneamines. They are sometimes referred to as alkylene polyamines or polyalkylene polyamines. These amines consist mainly of polyamines having the structure wherein R''' is a divalent aliphatic hydrocarbon group containing 2 to about 4 carbon atoms and p is an integer from 1 to 6. Representative examples are ethylenediamine, 1, 2-propylenediamine, 1, 2-butylenediamine, 1, 3-propanediamine, diethylenetriamine, triethylene tetramine, tetraethylene pentamine (TEPA), pentaethylene hexamine, hexaethylenehaptamine and the like. Of these, the most preferred are the polyethyleneamines containing 2 to 6 ethylene amine units such as diethylene triamine, triethylene tetramine, tetraethylene pentamine, and the like, including mixtures thereof.
  • Reaction of the alkylene oxide with the amine forms hydroxyalkyl groups having the formula wherein R' is a divalent aliphatic hydrocarbon group containing 2 to 4 carbon atoms and p is an integer from 1 to 10. The value of p depends upon how many moles of alkylene oxide are reacted per mole of amine.
  • the amount of alkylene oxide reacted is sufficient to provide an average of 1-4 oxyalkylene units per molecule of amine.
  • the molecules of alkylene oxide reacted are at least one less than the number of equivalents of reactive amine groups in the amine.
  • a reactive group is one that has at least one hydrogen atom bonded to it - - in other words, primary or secondary amine groups.
  • one mole of ethylenediamine has two reactive amine groups and hence represents two equivalents.
  • one mole of tetraethylene pentamine is five equivalents. Therefore, one mole of ethylenediamine is preferably oxyalkylated with up to one mole of alkylene oxide.
  • one mole of tetraethylene pentamine is preferably oxyalkylated with up to 4 ; moles of alkylene oxide.
  • the minimum amount of alkylene oxide is 0 . 1 moles per mole of amine; more preferably, 0.5 mole of amine. Hence, the preferred amount is 0. 5-4 moles.
  • Oxyalkylation introduces hydroxyalkyl groups. Rather than carrying out the oxyalkylation of the amine, it is also possible to acquire hydroxyalkyl subsituted amines from comme rcial sources, and use these in making the succinic dispersant. This is considered equivalent.
  • boronating agent such as B 2 O 3 , boron acids such as H 3 BO 3 , lower alkyl esters of boron acids such as trimethylborate or triethylborate, boron halides such as BF 3 , or BCl 3 , salts of boron acids, such as sodiun borate, or ammonium borate and the like.
  • the most preferred boronating agent is boric acid.
  • the amount of boronating agent should be an amount sufficient to introduce at least 0. 001 weight percent boron into the succinimide product excluding inert diluent such as mineral oil.
  • the preferred amount of boron in the succinimide exclusive of diluent is 0. 001-2. 5 weight percent, more preferably 0. 005-0. 5 weight percent. Excess boronating agent can be used and any remaining unreacted can be removed by filtration.
  • the boronated succinimide dispersant can be made by reacting the aliphatic hydrocarbon-substituted succinic acid, anhydride or ester with the oxyalkylated amine and the bo ronating agent. These can be reacted in any sequence or altogether.
  • the boronating agent - can-be reacted with the oxyalkylated amine to form an intermediate which is then reacted with the succinic compound.
  • the boronating agent can first be reacted with the succinic compound to form an intermediate which is then reacted with the oxyalkylated amine.
  • the boronated succinimide dispersant is made by one of the following two procedures.
  • the hydrocarbon-substituted succinic compound preferably polybutenyl substitut ed succinic anhydride
  • the oxyalkylated amine preferably oxyethylated polethyleneamine
  • the boronating agent preferably boric acid
  • a mixture of all three reactants i. e. hydrocarbyl succinic compound, oxyalkylated amine and boronating agent
  • reactants i. e. hydrocarbyl succinic compound, oxyalkylated amine and boronating agent
  • the reaction temperature is not critical. Any temperature high enough to cause the reaction to proceed but no so high as to cause degradation of the reactants or products can be used.
  • a preferred temperature range for use in any of the different methods of making the boronated succinimide is
  • the aliphatic hydrocarbon-substituted succinic compound reacts with the oxyalkylated amine to form amides, imides, esters and mixtures thereof. These are referred to collectively herein as succinimides.
  • Imide formation can be shown by the following structure in which the remaining bond on nitrogen is bonded to the remaining part of the oxyalkylated amine.
  • Amide formation can be illustrated by the structure Likewise, ester formation involving the hydroxyalkyl group formed in the oxyalkylation can be shown as follows
  • the product is a mixture of imides, amides and esters with the majority of the product having succinimide units.
  • the second required component of the synergistic combination is the Mannich dispersant made from an aliphatic hydrocarbon-substituted phenol, an aldehyde, or aldehyde precursor and an amine having at least one primary or secondary amine group.
  • the methylene bridge(s) is (are) bonded to a nitrogen atom of the amine.
  • Such dispersants are well known as identified by the prior art patents noted above.
  • the Mannich dispersants are readily made starting with an aliphatic hydrocarbon-substituted phenol having the formula wherein R" and n are as previously defined. These compounds can be made by reacting an olefin having the proper molecular weight with phenol or a monoalkyl substituted phenol. The olefin should contain 50-500 carbon atoms which give a molecular weight of 700-7000.
  • the olefin reactant is preferably made by polymerizing a lower olefin such as ethylene propylene, isobutylene, a-hexene, ⁇ -octene and mixtures thereof.
  • useful olefin polymer reactants are polybutene, polypropylene, ethylene-propylene copolymer, and the like.
  • Terpolymers can also be used to introduce the aliphatic hydrocar- b on group. These include ethylene-propylene copolymers with dienes such as 1,4-hesadiene, 1, 3-hexadiene, 1, 4-cycloctadiene, dicyclopentadiene, and the like.
  • the more preferred aliphatic hydrocarbon-substituted phenol reactant is polybutenyl phenol made by reacting a polybutene of 700-7000 molecular weight with phenol using a BF 3 catalyst such as BF 3 phenate or etherate at 0-60°C.
  • a BF 3 catalyst such as BF 3 phenate or etherate at 0-60°C.
  • Some more preferred reactants are those in which the polybutenyl group has a molecular weight of 1000-3000.
  • the methylene bridge attached at one end to the phenol is introduced by reaction with an aldehyde such as formaldehyde or a formaldehyde precursor such as paraformaldehyde.
  • an aldehyde such as formaldehyde or a formaldehyde precursor such as paraformaldehyde.
  • One or two such bridges may form.
  • the other end of the methylene bridge is bonded to a nitrogen atom of an amine.
  • Preferred amines contain 1 to about 10 nitrogen atoms and 1 to about 30 carbon atoms. More preferred amines are aliphatic amines. Examples of such amines are methyl amine, ethyl amine, isobutyl amine, lauryl amine, oleyl amine, stearyl amine, eicosamine, tricontamine, N-propyl- ethylene diamine, N-dodecyl-1,3-propanediamine, N-(dodecyl aminoethyl) ethylene diamine, N-(eicosylaminoethyl) ethylenediamine, N-aminoethylpiperazine, N-aminopropyl piperidine, ethanol amine, N-aminoethylmorpholine, 1, 3-propane diamine, N, N-dimethyl-1,3-propanedia
  • a preferred class of amines for use in making the Mannich dispersants is the polyalkyleneamines which were also a preferred class of amines for use in making the succinimide dispersants. They have been previously described and exemplified.
  • Fatty acids useful in modifying the Mannich dispersants include the aliphatic carboxylic acids containing 4 to about 30 carbon atoms.
  • the more preferred fatty acids are those containing about 10-30 carbon atoms such as capric acid, undecylic acid, lauric acid, tridecoic acid, myristic acid, palmitic acid, linoleic acid, stearic acid, arachidic acid and the like.
  • the preferred fatty acid is oleic acid.
  • Boron compounds useful in modifying the Mannich dispersant are the same boron compounds used to boronate the succinimide dispersants. These are boron oxides, boron acids, esters of boron acids, salts of boron acids, boron halides, and mixtures thereof.
  • the preferred boronating . agent is boric acid. Use of such boronating agents in modifying Mannich dispersants is described in more detail in the hereinabove identified patents.
  • the Mannich dispersants are made by reacting about one mole of aliphatic hydrocarbon- substituted phenol, 0. 9-2. 5 moles of formaldehyde or formaldehyde precursors, 0. 1-2. 0 moles of amine, 0 to 3 moles of fatty acid and 0 to 2. 0 moles of boronating agent. These can be reacted in any order or altogether.
  • the Mannich dispersant is made by heating a mixture of aliphatic hydrocarbon substituted phenol and amine at 60-200°C. and adding a formaldehyde to the heated mixture to form a Mannich condensate. If boronated Mannich is used the boronating agent (e. g.
  • boric acid can be added subsequently to the mixture and heating to 100-250°C. as the desired amount of boron is introduced.
  • part of the Mannich condensate can be segregated and heated with a boronating agent (e. g. boric acid) to introduce a higher level of boron than is desired in the final Mannich.
  • a boronating agent e. g. boric acid
  • This overboronated product can then be blended back into the unboronated Mannich to achieve the desired boron level.
  • the final Mannich can be clarified by filtration.
  • Fatty acid modified Mannich dispersants can be made by heating a mixture of aliphatic hydrocarbon-substituted phenol, formaldehyde, amine and fatty acid to 50 to 150*C. More preferably, the formaldehyde is withheld and added slowly to a mixture of the other reactants while stirring at 50-150°C.
  • the Mannich dispersant can be modified with both boron and fatty acid. This can readily be accomplished by combining the foregoing procedures For example, one can heat a mixture of hydrocarbon-substituted phenol (e.g. polybutenyl phenol), amine(e. g. tetraethylene pentamine) and fatty acid (e. g. oleic acid) to reaction temperature and then add formaldehyde and subsequently a boronating agent (e. g. boric acid). Alternatively, one can form a mixture of hydrocarbon-substituted phenol, amine, boronating agent and fatty acid and add formaldehyde to the heated mixture.
  • hydrocarbon-substituted phenol e.g. polybutenyl phenol
  • amine(e. g. tetraethylene pentamine) and fatty acid e. g. oleic acid
  • formaldehyde e.g. oleic acid
  • the Mannich condensate of hydrocarbon-substituted phenol formaldehyde and amine is split into separate portions. One portion is heated with a boronating agent such as boric acid and the second portion is heated with a fatty acid such as oleic acid to obtain two separate modified intermediate products.
  • a boronating agent such as boric acid
  • a fatty acid such as oleic acid
  • Mannich condensate which is both boron and fatty acid modified.
  • Other reaction sequences involving the condensation of hydrocarbon-substituted phenol, amine, formaldehyde, boronating agent, and fatty acid will be apparent to the average chemist.
  • Mannich dispersants can be made following the above general procedure by substituting any of the previously disclosed primary and secondary amines in place of N, N-dimethyl- 1, 3-propanediamine.
  • tetraethylene pentamine on an equal mole basis yields an effective dispersant which may be readily modified by heating with boric acid and/or oleic acid to improve its properties, especially with regard to corrosiveness.
  • Each of the two types of synergistic additives is used in lubricating oil at a concentration which maximizes their total effectiveness at an acceptable cost.
  • a useful concentration range for each is 0. 05-10 weight percent.
  • a more preferred range is 0. 5-5 weight percent and a highly preferred range is 1-3 weight percent.
  • These concentrations do not include any mineral oil diluent incorporated into the additive during manufacture.
  • the additives can be used in mineral oil or in synthetic oils of viscosity suitable for use in the crankcase of an internal combustion engine.
  • Crankcase lubricating oils have a viscosity up to about 0.0000159m 2 /sec. at 210°F.
  • Crankcase lubricating oils of the present invention have a viscosity up to about SAE 50. Sometimes such motor oils are given a classification at both 0° and 210°F., such as SAE 10W 40 or SAE 5W 30.
  • Mineral oils include those of suitable viscosity refined from crude oil from sources including Gulfcoast, midcontinet, Pennsylvania, mideast, California, Alaska, North Sea, and the like. Various standard refinery operations can be used in processing the mineral oil.
  • Synthetic oil includes both hydrocarbon synthetic oil and synthetic esters.
  • Useful synthetic hydrocarbon oils include liquid polymers of a-olefins having the proper viscosity. Especially useful are the hydrogenated liquid oligomers of C 6-12 a-olefins such as a-decene trimer. Likewise, alkylbenzenes of proper viscosity can be used, such as didodecylbenzene.
  • Useful synthetic esters include the esters of both monocarboxylic acid and polycarboxylic acid as well as monohydroxy alkanols and polyols. Typical examples are didodecyl adipate, trimethylol propane tripelargonate, pentaerythritol tetracaproate, di-(2-ethylhexyl)adipate, dilauryl sebacate and the like. Complex esters prepared from mixtures of mono- and dicarboxylic acid and mono- and polyhydroxyl alkanols can also be used.
  • Blends of mineral oil with synthetic oil are particularly useful. For example, blends of 10-25 weight percent hydrogenated a-decene trimer with 75-90 weight percent 0.0000321 m 2 /sec. (100°F.) mineral oil results in an excellent lubricant. Likewise, blends of about 10-25 weight percent di(2-ethylhexyl)adipate with mineral oil of proper viscosity results in a superior lubricating oil. Also blends of synthetic hydrocarbon oil with synthetic esters can be used. Blends of mineral oil with synthetic oil are especially useful when preparing low viscosity oil (e. g. SAE 5W 20) since they permit these low viscosities without contributiong excessive volatility.
  • low viscosity oil e. g. SAE 5W 20
  • the more preferred lubricating oil composition includes zinc dihydrocarbyldithiophosphate (ZDDP) in combination with the present additives
  • ZDDP zinc dihydrocarbyldithiophosphate
  • a typical alkyl-type ZDDP contains a mixture of isobutyl and isoamyl groups.
  • Zinc di-(nonylphenyl)dithiophosphate is a typical aryl-type ZDDP. Good results are achieved using sufficient ZDDP to provide 0. 01-0. 5 weight percent zinc. A preferred concentration supplies 0. 025-0. 3 weight percent zinc.
  • alkaline earth metal petroleum sulfonates or alkaline earth metal alkaryl sulfonates are the alkaline earth metal petroleum sulfonates or alkaline earth metal alkaryl sulfonates.
  • examples of these are calcium petroleum sulfonates, magnesium petroleum sulfonates, barium alkaryl sulfonates, calcium alkaryl sulfonates or magnesium alkaryl sulfonates.
  • Both the neutral and the overbased sulfonates having base numbers up to about 400 can be beneficially used. These are used in an amount to provide 0. 05-1. 5 weight percent alkaline earth metal and more preferably 0. 1-1. 0 weight percent.
  • the lubricating oil composition contains a calcium and/or magnesium petroleum sulfonate or alkaryl (e. g. alkylbenzene) sulfonate.)
  • viscosity index improvers can be included such as the polyalkylmethacrylate type or the ethylene-propylene or ethylene-propylene- dienecopolymer type.
  • styrene-diene VI improvers or styrene-acrylate copolymers can be used.
  • Alkaline earth metal salts of phosphosulfurized polyisobutylene are useful.
  • Tests were conducted which demonstrated the substantial synergistic effect of the present invention.
  • the test used was industry- recognized ASTM Sequence VD engine test. In this test, a Ford Pinto engine is operated on a fixed schedule with the test oil in the engine crankcase. After the operating schedule is complete, the engine is disassembled and various parts rated for cleanliness using a standard rating scale of 1-10 in which 10 is clean.
  • the base test oil was a fully formulated mineral oil. The only difference between the test oils was the dispersant. The dispersant varied as follows: The test results are shown in the following table:
  • Oil C containing the synergistic combination gave a much better average varnish and piston varnish rating at 5 percent total dispersant than either Oil A or Oil B using the same individual components separately and at a much higher concentration. Hence, the combination gives results superior to the sum of the expected contributions of the components.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)

Abstract

Lubricating oil dispersancy is improved by the use of a novel composition comprising a synergistic mixture of a boronated hydrocarbon-substituted succinic amide/imide/ ester of an oxyalkylated amine and a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and an amine, and, optionally, a fatty acid and/or a boronating agent. The invention includes such compositions, the ingredients of such a composition when intended for such use, lubricating oil compositions containing the same ingredients, a method of improving lubricating oil dispersancy using the same ingredients and additive packages for lubricating oil using the same ingredients.

Description

  • This invention relates to a dispersant canposition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture.
  • Dispersants are used in engine lubricating oil to prevent sludge formation and to inhibit varnish on hot engine surfaces such as pistons. Hydrocarbon-substituted succinimides are quite effective in such use (U.S. Patent 3,172,892). Likewise, succinimides of hydroxyalkyl substituted amines have been shown to be effective (U.S. Patent 3,219,666). Boronation of such succinimides has also been practiced (U.S. Patents 3,322,670; 3,254,025 and 3,087,936). Boronation processes are also taught in U.S. Patents 3,082,955; 3,950,341 and 3,089,936.
  • Mannich dispersants made fran hydrocarbon-substituted phenols, formaldehyde and amines are also known (U.S. Patents 3,413,347; 3,725,277; 3,368,972 and 3,798,165). Boron-modified Mannich dispersant are described in U.S. Patents 3,697,574; 3,703,536; 3,704,308; 3,751,365; and 3,756,953. Fatty acid modified Mannich dispersants are described in U.S. Patents 3,798,247 and 3,803,039. Further representative U.S. patents include the following:-
    Figure imgb0001
    and in addition, reference can be made to British Patent 1,362,013
  • According to the present invention dispersant compositions are provided which contain a synergistic mixture of (a) a boronated hydrocarbon-substituted succinic amide/imide/ester of an oxyalkylated anine and (b) a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and an anine, and, optionally, a boronating agent and/or fatty acid . These compositions may be added to lubricating oil (or the ingredients thereof may be so-added separately). In a standard ASIM Sequence VD engine test, the synergistic canbination gives a much better piston varnish rating than either individual component used at the. same or even greater total concentration.
  • A preferred embodiment of the invention is a lubricating oil composition comprising a major amount of an oil of lubricating viscosity containing a minor dispersant amount of a synergistic combination of dispersants, said combination comprising
    • (A) a boronated succinimide dispersant having in its structure at least one aliphatic hydrocarbon-substituted succinoyl group
      Figure imgb0002
      wherein R is an aliphatic hydrocarbon group having a molecular weight of 700-50, 000, said succinoyl group being bonded to a nitrogen atom of an oxyalkylated amine to form an amide or imide or to an oxygen atom of said oxyalkylated amine to form an ester or to both nitrogen and oxygen atorns of said oxyalkylated amine to form a mixture containing amide, imide and ester groups, said succinimide dispersant being further characterized by containing 0. 001-2. 5 weight percent boron, and
    • (B) a Mannich dispersant having in its structure an aliphatic hydrocarbon- substituted phenolic group
      Figure imgb0003
      wherein R" is an aliphatic hydrocarbon group containing 1 to 500 carbon atoms and n is 1 or 2, m is 0 or 1, n m is 1 or 2, at least one of said R'' groups being an aliphatic hydrocarbon group containing 50-500 carbon atoms, said phenolic group being bonded through a methylene group to a nitrogen atom of an amine, said amine containing 1 to 10 nitrogen atoms and 1 to 30 carbon atoms.
  • The invention also provides a boronated hydrocarbon- substituted succinic amide/imide and/or ester of an oxyalkylated amine or a Mannich condensation product of a hydrocarbon-substituted phenol, fonnaldeyhyde and an amine, and, optionally a boronating agent and/or a fatty acid, in either case intended for use in a synergistic dispersant mixture comprising at least one representative of each of the aforesaid dispersants.
  • Several examples of the boronated succinimide dispersant are known in the prior art identified above. The boronated succinimide dispersant can be made by reacting an aliphatic hydrocarbon-substituted succinic acid anhydride or lower alkyl ester with an oxyalkylated amine and a boronating agent in the approximate mole ratio of 1.0:0.2-2, 0:001-5.0.
  • The preferred succinic reactant is an aliphatic hydrocarbon-substituted succinic anhydride in which the aliphatic hydrocarbon group has a molecular weight of 700-50, 000. The aliphatic hydrocarbon group is preferably derived from an olefin polymer such as polypropylene, polybutene, ethylene-propylene copolymer, ethylene-propylene-1, 4-hexadiene copolymer ethylene-propylene-1,4-cyclohexadiene copolymer, ethylene-propylene-1,5-cycloctadiene copolymer, ethylene-propylene-5-methylene-2-norbomene, or etylene-propplene-2, 5-norbornadiene copolymer.
  • The most preferred aliphatic hydrocarbon substituent is derived from an olefin polymer having a molecular weight of 700-5000. These include the olefin polymers mentioned above which have the more preferred molecular weight. Of the above, polybutene is most preferred. Optionally, a high molecular weight of olefin polymer, for example, one having a molecular weight of 50, 000 or more can be degraded to produce an olefin polymer having a more preferred molecular weight. Methods of reducing the carbon chain length of olefin polymers by shearing are well known. Mere heating with mechanical stirring will reduce molecular weight. Air can be injected into heated polymer to cause degradation and reduce molecular weight. Extrusion through an orifice under pressure causes chain scission. Any combination of such methods can be used.
  • Highly preferred olefin polymers for use in making the succinic substituent are polymers of butene. Of these, the most preferred are the polybutenes having an average molecular weight of 700-2000.
  • The hydrocarbon substituent can be introduced by heating a mixture containing the olefin polymer and maleic anhydride to 200-250°C. The reaction can be catalyzed by injecting chlorine. Likewise, a peroxide catalyst can be used. The reaction is preferably conducted in a mineral oil diluent which can remain in the succinic product to act as a.solvent in later stages of the preparation. The aliphatic hydrocarbon-substituted succinic anhydrides are well known.
  • The oxyalkylated amines are readily made by reacting an alkylene oxide with an amine having primary and/or secondary amine groups. The preferred alkylene oxides are ethylene oxide, propylene oxide, and butylene oxide. The more preferred are ethylene oxide, and propylene oxide or mixtures thereof. The most preferred oxyalkylating agent is ethylene oxide.
  • The amines which are oxyalkylated are those containing 2 to 10 nitrogen atoms. More preferably, they also contain about 2-20 carbon atoms. Some examples of these amines are ethylenediamine, 1, 2-propylene- diamine, 1, 3-propanediamine, N-aminoethyl piperazine, N-oleylaminopropyl-1, 3-propane diamine, diethylene triamine, triethylene tetramine, tetraethylene pentamine, pentaethylene hexamine, N-dodecyl ethylenediamine, N-dodecyl- 1, 3-propane diamine, N-octadecyl diamine, N-(decylaminoethyl) ethylenediamine and the like.
  • The preferred amines for use in making the succinic dispersants are the polyalkyleneamines. They are sometimes referred to as alkylene polyamines or polyalkylene polyamines. These amines consist mainly of polyamines having the structure
    Figure imgb0004
    wherein R''' is a divalent aliphatic hydrocarbon group containing 2 to about 4 carbon atoms and p is an integer from 1 to 6. Representative examples are ethylenediamine, 1, 2-propylenediamine, 1, 2-butylenediamine, 1, 3-propanediamine, diethylenetriamine, triethylene tetramine, tetraethylene pentamine (TEPA), pentaethylene hexamine, hexaethylenehaptamine and the like. Of these, the most preferred are the polyethyleneamines containing 2 to 6 ethylene amine units such as diethylene triamine, triethylene tetramine, tetraethylene pentamine, and the like, including mixtures thereof.
  • Reaction of the alkylene oxide with the amine forms hydroxyalkyl groups having the formula
    Figure imgb0005
    wherein R' is a divalent aliphatic hydrocarbon group containing 2 to 4 carbon atoms and p is an integer from 1 to 10. The value of p depends upon how many moles of alkylene oxide are reacted per mole of amine.
  • Preferably, the amount of alkylene oxide reacted is sufficient to provide an average of 1-4 oxyalkylene units per molecule of amine.
  • More preferably, the molecules of alkylene oxide reacted are at least one less than the number of equivalents of reactive amine groups in the amine. A reactive group is one that has at least one hydrogen atom bonded to it -- in other words, primary or secondary amine groups. For example, one mole of ethylenediamine has two reactive amine groups and hence represents two equivalents. Likewise, one mole of tetraethylene pentamine is five equivalents. Therefore, one mole of ethylenediamine is preferably oxyalkylated with up to one mole of alkylene oxide. Likewise, one mole of tetraethylene pentamine is preferably oxyalkylated with up to 4 ; moles of alkylene oxide. The minimum amount of alkylene oxide is 0. 1 moles per mole of amine; more preferably, 0.5 mole of amine. Hence, the preferred amount is 0. 5-4 moles.
  • Oxyalkylation introduces hydroxyalkyl groups. Rather than carrying out the oxyalkylation of the amine, it is also possible to acquire hydroxyalkyl subsituted amines from comme rcial sources, and use these in making the succinic dispersant. This is considered equivalent.
  • Boron is introduced into the succinimide additive by use of a boronating agent as is shown in the patents identified above. Suitable boronating agents include any boron compound that will serve to introduce boron into the succinimide and not adversely affect the dispersant properties of the additive cambination. Useful boronating agents include boron oxides such as B2O3, boron acids such as H3BO3, lower alkyl esters of boron acids such as trimethylborate or triethylborate, boron halides such as BF3, or BCl3, salts of boron acids, such as sodiun borate, or ammonium borate and the like. The most preferred boronating agent is boric acid.
  • The amount of boronating agent should be an amount sufficient to introduce at least 0. 001 weight percent boron into the succinimide product excluding inert diluent such as mineral oil. The preferred amount of boron in the succinimide exclusive of diluent is 0. 001-2. 5 weight percent, more preferably 0. 005-0. 5 weight percent. Excess boronating agent can be used and any remaining unreacted can be removed by filtration.
  • The boronated succinimide dispersant can be made by reacting the aliphatic hydrocarbon-substituted succinic acid, anhydride or ester with the oxyalkylated amine and the boronating agent. These can be reacted in any sequence or altogether. For example, the boronating agent - can-be reacted with the oxyalkylated amine to form an intermediate which is then reacted with the succinic compound. Alternatively, the boronating agent can first be reacted with the succinic compound to form an intermediate which is then reacted with the oxyalkylated amine.
  • More preferably, the boronated succinimide dispersant is made by one of the following two procedures. In the first procedure, the hydrocarbon-substituted succinic compound (preferably polybutenyl substitut ed succinic anhydride) is reacted with the oxyalkylated amine (preferably oxyethylated polethyleneamine) to form an intermediate which is then reacted with the boronating agent (preferably boric acid).
  • In a second more preferable procedure, a mixture of all three reactants (i. e. hydrocarbyl succinic compound, oxyalkylated amine and boronating agent) is formed and heated to react all at once.
  • The reaction temperature is not critical. Any temperature high enough to cause the reaction to proceed but no so high as to cause degradation of the reactants or products can be used. A preferred temperature range for use in any of the different methods of making the boronated succinimide is
  • 100-300°C., more preferably, 150-250°C.
  • The aliphatic hydrocarbon-substituted succinic compound reacts with the oxyalkylated amine to form amides, imides, esters and mixtures thereof. These are referred to collectively herein as succinimides. Imide formation can be shown by the following structure
    Figure imgb0006
    in which the remaining bond on nitrogen is bonded to the remaining part of the oxyalkylated amine. Amide formation can be illustrated by the structure
    Figure imgb0007
    Likewise, ester formation involving the hydroxyalkyl group formed in the oxyalkylation can be shown as follows
    Figure imgb0008
  • In practice, the product is a mixture of imides, amides and esters with the majority of the product having succinimide units.
  • The second required component of the synergistic combination is the Mannich dispersant made from an aliphatic hydrocarbon-substituted phenol, an aldehyde, or aldehyde precursor and an amine having at least one primary or secondary amine group. This leads: to a Mannich condensate which can be defined by the presence within its structure of an aliphatic hydrocarbon-substituted phenolic group having the formula
    Figure imgb0009
    wherein R" is an aliphatic hydrocarbon group containing one to about 500 carbon atoms, and n is one or two, m is 0 or 1 and n + m is 1 or 2. At least one R" group contains about 50-500 carbon atoms. The methylene bridge(s) is (are) bonded to a nitrogen atom of the amine. Such dispersants are well known as identified by the prior art patents noted above.
  • The Mannich dispersants are readily made starting with an aliphatic hydrocarbon-substituted phenol having the formula
    Figure imgb0010
    wherein R" and n are as previously defined. These compounds can be made by reacting an olefin having the proper molecular weight with phenol or a monoalkyl substituted phenol. The olefin should contain 50-500 carbon atoms which give a molecular weight of 700-7000. The olefin reactant is preferably made by polymerizing a lower olefin such as ethylene propylene, isobutylene, a-hexene, α-octene and mixtures thereof. Thus, useful olefin polymer reactants are polybutene, polypropylene, ethylene-propylene copolymer, and the like. Terpolymers can also be used to introduce the aliphatic hydrocar- bon group. These include ethylene-propylene copolymers with dienes such as 1,4-hesadiene, 1, 3-hexadiene, 1, 4-cycloctadiene, dicyclopentadiene, and the like.
  • The more preferred aliphatic hydrocarbon-substituted phenol reactant is polybutenyl phenol made by reacting a polybutene of 700-7000 molecular weight with phenol using a BF3 catalyst such as BF3 phenate or etherate at 0-60°C. Some more preferred reactants are those in which the polybutenyl group has a molecular weight of 1000-3000.
  • The methylene bridge attached at one end to the phenol is introduced by reaction with an aldehyde such as formaldehyde or a formaldehyde precursor such as paraformaldehyde. One or two such bridges may form.
  • The other end of the methylene bridge is bonded to a nitrogen atom of an amine. Preferred amines contain 1 to about 10 nitrogen atoms and 1 to about 30 carbon atoms. More preferred amines are aliphatic amines. Examples of such amines are methyl amine, ethyl amine, isobutyl amine, lauryl amine, oleyl amine, stearyl amine, eicosamine, tricontamine, N-propyl- ethylene diamine, N-dodecyl-1,3-propanediamine, N-(dodecyl aminoethyl) ethylene diamine, N-(eicosylaminoethyl) ethylenediamine, N-aminoethylpiperazine, N-aminopropyl piperidine, ethanol amine, N-aminoethylmorpholine, 1, 3-propane diamine, N, N-dimethyl-1,3-propanediamine, 1,6-hexane diamine and the like.
  • A preferred class of amines for use in making the Mannich dispersants is the polyalkyleneamines which were also a preferred class of amines for use in making the succinimide dispersants. They have been previously described and exemplified.
  • Fatty acids useful in modifying the Mannich dispersants include the aliphatic carboxylic acids containing 4 to about 30 carbon atoms. The more preferred fatty acids are those containing about 10-30 carbon atoms such as capric acid, undecylic acid, lauric acid, tridecoic acid, myristic acid, palmitic acid, linoleic acid, stearic acid, arachidic acid and the like. The preferred fatty acid is oleic acid. The use of such fatty acids in modifying Mannich dispersants is described in more detail in the above-identified patents.
  • Boron compounds useful in modifying the Mannich dispersant are the same boron compounds used to boronate the succinimide dispersants. These are boron oxides, boron acids, esters of boron acids, salts of boron acids, boron halides, and mixtures thereof. The preferred boronating . agent is boric acid. Use of such boronating agents in modifying Mannich dispersants is described in more detail in the hereinabove identified patents.
  • The Mannich dispersants are made by reacting about one mole of aliphatic hydrocarbon- substituted phenol, 0. 9-2. 5 moles of formaldehyde or formaldehyde precursors, 0. 1-2. 0 moles of amine, 0 to 3 moles of fatty acid and 0 to 2. 0 moles of boronating agent. These can be reacted in any order or altogether. In a preferred method, the Mannich dispersant is made by heating a mixture of aliphatic hydrocarbon substituted phenol and amine at 60-200°C. and adding a formaldehyde to the heated mixture to form a Mannich condensate. If boronated Mannich is used the boronating agent (e. g. boric acid) can be added subsequently to the mixture and heating to 100-250°C. as the desired amount of boron is introduced. Alternatively, part of the Mannich condensate can be segregated and heated with a boronating agent (e. g. boric acid) to introduce a higher level of boron than is desired in the final Mannich. This overboronated product can then be blended back into the unboronated Mannich to achieve the desired boron level. The final Mannich can be clarified by filtration.
  • Fatty acid modified Mannich dispersants can be made by heating a mixture of aliphatic hydrocarbon-substituted phenol, formaldehyde, amine and fatty acid to 50 to 150*C. More preferably, the formaldehyde is withheld and added slowly to a mixture of the other reactants while stirring at 50-150°C.
  • The Mannich dispersant can be modified with both boron and fatty acid. This can readily be accomplished by combining the foregoing procedures For example, one can heat a mixture of hydrocarbon-substituted phenol (e.g. polybutenyl phenol), amine(e. g. tetraethylene pentamine) and fatty acid (e. g. oleic acid) to reaction temperature and then add formaldehyde and subsequently a boronating agent (e. g. boric acid). Alternatively, one can form a mixture of hydrocarbon-substituted phenol, amine, boronating agent and fatty acid and add formaldehyde to the heated mixture. In another procedure, the Mannich condensate of hydrocarbon-substituted phenol formaldehyde and amine is split into separate portions. One portion is heated with a boronating agent such as boric acid and the second portion is heated with a fatty acid such as oleic acid to obtain two separate modified intermediate products.
  • These products can then be blended back together to obtain a Mannich condensate which is both boron and fatty acid modified. Other reaction sequences involving the condensation of hydrocarbon-substituted phenol, amine, formaldehyde, boronating agent, and fatty acid will be apparent to the average chemist.
  • The following Preparations 1 to 4 illustrate the preparation of the succinimide type dispersants.
  • PREPARATION 1
  • In a reaction vessel was placed 1080 grams (6. 0 moles) of a mixture of polyethyleneamine having an average composition corresponding to tetraethylene pentamine. This was stirred under nitrogen and heated to about 120°C. Then 441 grams (10. 0 moles) of ethylene oxide was injected over a 3. 5 hour period to form an oxyethylated polyethyleneamine.
  • In a second reaction vessel was placed 101. 6 grams (about 0.4 moles) of the above oxyethylated polyethyleneamine, 28. 8 grams (0.47 moles of boric acid, 9. 6 grams of water and 727 grams (about 0. 6 moles) of a polybutenyl succinic anhydride. This mixture was stirred under nitrogen and heated to 175°C. over a three hour period. It was then stirred for an additional hour at 175°C. while vacuum was applied to remove residual water. The product was diluted with one-half its weight of mineral oil to be 67 percent active dispersant. It was clarified by filtration. Analysis gave amine number 0. 85, acid number 0.09, nitrogen 1. 84 wei ght percent, boron 0. 3 weight percent.
  • PREPARATION 2
  • In a reaction vessel was placed 1124 grams (1.3 moles) of polyisobutenyl succinic anhydride and 254 grams (1. 0 mole) of oxyethylated polyethyleneamine made by reacting about 1. 67 moles of ethylene oxide with one mole of poly ethyleneamine having an average molecular weight of 180. This mixture was heated under nitrogen to 175°C. while bubbling nitrogen through the liquid and maintaining a vacuum of about 26. 5 inches (Hg) for 4. 5 hours. The resultant product was diluted with mineral oil to give a 67 percent active material. Then 75 grams (1. 2 moles) of boric acid and 25 grams of water were added. The mixture was heated to 100°C. and nitrogen was bubbled through it for three hours. It was then heated to 150°C. and nitrogen sparge continued for two hours. The product was filtered to obtain a clear boronated succinimide dispersant for use in the synergistic combination. It analyzed 2.42 weight percent nitrogen, 0.49 weight percent boron, amine number 1.16 total base number 34.4 and acid number 0.03.
  • PREPARATION 3
  • In a reaction vessel was placed 396 grams (2. 2 moles) of polyethyleneamine having an average composition corresponding to tetraethylene pentamine. This was heated to 120°C. and 162 .grams (3. 7 moles) of ethylene oxide was injected into the amine at 120-140 over a 2. 5 hour period.
  • In a second reaction vessel was placed 254 grams (aboct 1 mole) of an oxyethylated polyethyleneamine, 93 grams (1. 5 moles) boric acid and 47 grams of water. This was stirred at 100°C. with nitrogen sparge for three hours. It was then heated to 150°C. and nitrogen sparge continued for two hours to obtain a boronated-oxyethylated polyethyleneamine.
  • In another reaction vessel was placed 1798 grams (1. 6 moles)of polybutenyl succinic anhydride and 222 (0. 75 moles) of the above boronated-oxyethylated polyethyleneamine. This mixture was placed under vacuum with nitrogen sparge and heated to 175°C. for 4. 5 hours. The product was diluted with mineral oil to be 67 percent active. It analyzed 0. 2 weight percent boron.
  • PREPARATION 4
  • In a reaction vessel was placed 1487 grams ( 1. 6 moles) of polybutenyl succinic anhydride, 74 grams (1. 5 moles) boric acid and 24 grams of water. This mixture was stirred and heated under nitrogen at 100°C. for three hours, and then at 150 °C. under vacuum for two hours. To this was then added 203 grams (0. 8 mole) of an oxyethylated polyethyleneamine made by reacting 1. 67 moles of ethylene oxide with 1 mole of polyethyleneamine having the average composition of a tetraethylene pentamine. This mixture was heated at 175°C. with nitrogen sparge under vacuum for 4. 5 hours. The final product was diluted with one-half its weight in process oil to give a 67 percent active product and analyzed 0. 13 weight percent boron.
  • The following Preparation illustrates a method for making the Mannich dispersants.
  • PREPARATION 5
  • In a reaction vessel was placed 2019 grams of heptane, 529. 7 grams of polybutene (mole weight 1000) and 79. 5 grams of phenol. To this was added 23. 9 grams of BF3 phenate over a 20-minute period at 40°C. The mixture was then stirred for 90 minutes at 40°C. It was then washed at 60-70°C. with aqueous ammonia and then with water and finally with methanol, leaving behind the polybutenyl phenol. This was cooled to about 40°C. and 59 grams of N, N-dimethyl-1, 3-propanediamine was added and stirred. Then 27. 2 grams of formaldehyde was added incrementally over a 30-minute period at 40-50°C. Stirring was continued for 30 minutes and then the mixture was heated to about 130°C. while distilling out volatiles. It was stirred three hours at 130°C. under slight nitrogen pressure and then heated to 170°C. and vacuum applied to 50 mm. Hg. abs to complete removal of volatiles. It was then diluted with about 380 grams of hydrocarbon solvent and cooled giving a Mannich dispersant useful in the present combination.
  • Other Mannich dispersants can be made following the above general procedure by substituting any of the previously disclosed primary and secondary amines in place of N, N-dimethyl- 1, 3-propanediamine. For example, tetraethylene pentamine on an equal mole basis yields an effective dispersant which may be readily modified by heating with boric acid and/or oleic acid to improve its properties, especially with regard to corrosiveness.
  • Each of the two types of synergistic additives is used in lubricating oil at a concentration which maximizes their total effectiveness at an acceptable cost. A useful concentration range for each is 0. 05-10 weight percent. A more preferred range is 0. 5-5 weight percent and a highly preferred range is 1-3 weight percent. These concentrations do not include any mineral oil diluent incorporated into the additive during manufacture.
  • The additives can be used in mineral oil or in synthetic oils of viscosity suitable for use in the crankcase of an internal combustion engine. Crankcase lubricating oils have a viscosity up to about 0.0000159m2/sec. at 210°F.
  • Crankcase lubricating oils of the present invention have a viscosity up to about SAE 50. Sometimes such motor oils are given a classification at both 0° and 210°F., such as SAE 10W 40 or SAE 5W 30.
  • Mineral oils include those of suitable viscosity refined from crude oil from sources including Gulfcoast, midcontinet, Pennsylvania, mideast, California, Alaska, North Sea, and the like. Various standard refinery operations can be used in processing the mineral oil.
  • Synthetic oil includes both hydrocarbon synthetic oil and synthetic esters. Useful synthetic hydrocarbon oils include liquid polymers of a-olefins having the proper viscosity. Especially useful are the hydrogenated liquid oligomers of C6-12 a-olefins such as a-decene trimer. Likewise, alkylbenzenes of proper viscosity can be used, such as didodecylbenzene.
  • Useful synthetic esters include the esters of both monocarboxylic acid and polycarboxylic acid as well as monohydroxy alkanols and polyols. Typical examples are didodecyl adipate, trimethylol propane tripelargonate, pentaerythritol tetracaproate, di-(2-ethylhexyl)adipate, dilauryl sebacate and the like. Complex esters prepared from mixtures of mono- and dicarboxylic acid and mono- and polyhydroxyl alkanols can also be used.
  • Blends of mineral oil with synthetic oil are particularly useful. For example, blends of 10-25 weight percent hydrogenated a-decene trimer with 75-90 weight percent 0.0000321 m2/sec. (100°F.) mineral oil results in an excellent lubricant. Likewise, blends of about 10-25 weight percent di(2-ethylhexyl)adipate with mineral oil of proper viscosity results in a superior lubricating oil. Also blends of synthetic hydrocarbon oil with synthetic esters can be used. Blends of mineral oil with synthetic oil are especially useful when preparing low viscosity oil (e. g. SAE 5W 20) since they permit these low viscosities without contributiong excessive volatility.
  • The more preferred lubricating oil composition includes zinc dihydrocarbyldithiophosphate (ZDDP) in combination with the present additives Both zinc dialkyldithiophosphates and zinc dialksryldithiophosphates as well as mixed alkyl-aryl ZDDP are useful. A typical alkyl-type ZDDP contains a mixture of isobutyl and isoamyl groups. Zinc di-(nonylphenyl)dithiophosphate is a typical aryl-type ZDDP. Good results are achieved using sufficient ZDDP to provide 0. 01-0. 5 weight percent zinc. A preferred concentration supplies 0. 025-0. 3 weight percent zinc.
  • Another additive used in the oil compositions are the alkaline earth metal petroleum sulfonates or alkaline earth metal alkaryl sulfonates. Examples of these are calcium petroleum sulfonates, magnesium petroleum sulfonates, barium alkaryl sulfonates, calcium alkaryl sulfonates or magnesium alkaryl sulfonates. Both the neutral and the overbased sulfonates having base numbers up to about 400 can be beneficially used. These are used in an amount to provide 0. 05-1. 5 weight percent alkaline earth metal and more preferably 0. 1-1. 0 weight percent. In a most preferred embodiment the lubricating oil composition contains a calcium and/or magnesium petroleum sulfonate or alkaryl (e. g. alkylbenzene) sulfonate.)
  • Other viscosity index improvers can be included such as the polyalkylmethacrylate type or the ethylene-propylene or ethylene-propylene- dienecopolymer type. Likewise, styrene-diene VI improvers or styrene-acrylate copolymers can be used. Alkaline earth metal salts of phosphosulfurized polyisobutylene are useful.
  • Tests were conducted which demonstrated the substantial synergistic effect of the present invention. The test used was industry- recognized ASTM Sequence VD engine test. In this test, a Ford Pinto engine is operated on a fixed schedule with the test oil in the engine crankcase. After the operating schedule is complete, the engine is disassembled and various parts rated for cleanliness using a standard rating scale of 1-10 in which 10 is clean.
  • The base test oil was a fully formulated mineral oil. The only difference between the test oils was the dispersant. The dispersant varied as follows:
    Figure imgb0011
    The test results are shown in the following table:
    Figure imgb0012
  • Note that Oil C containing the synergistic combination gave a much better average varnish and piston varnish rating at 5 percent total dispersant than either Oil A or Oil B using the same individual components separately and at a much higher concentration. Hence, the combination gives results superior to the sum of the expected contributions of the components.

Claims (19)

1. A dispersant composition for lubricating oil comprising a mixture of a boronated hydrocarbon-substituted succinic amide/imide and/or ester of an oxyalkylated amine and a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and or amine, and, optionally a boronating agent and/or a fatty acid.
2. A composition as claimed in claim 1 and comprising a synergistic mixture of
(A) a boronated dispersant having in its structure at least one substituted succinoyl group
Figure imgb0013
wherein R is an aliphatic hydrocarbon group having a molecular weight of 700-50,000, the succinoyl group being bonded to a nitrogen atom of an oxyalkylated amine so as to form an amide or imide or to an oxygen atom of the oxyalkylated anine to form an ester or to both nitrogen and oxygen atoms of the oxyalkylated amine to form a mixture containing amide, imide, and/or ester groups, the boronated dispersant containing 0.001-2.5 weight percent boron; and
(B) a Mannich dispersant having in its structure a phenolic group
Figure imgb0014
wherein R" is an aliphatic hydrocarbon group containing 1 to 500 carbon atoms and n is 1 or 2, m is 0 or 1, and n + m is 1 or 2, at least one group R" being an aliphatic hydrocarbon group containing 50-500 carbon atoms, the phenolic group being bonded through a methylene group to a nitrogen atom of an amine containing 1 to 10 nitrogen atoms and 1 to 30 carbon atoms.
3. A composition as claimed in claim 2, wherein R is derived from an olefin polymer.
4. A composition as claimed in claim 2 or claim 3, wherein at least one group R" is derived fran an olefin polymer containing 50-500 carbon atoms.
5. A composition as claimed in claim 4, wherein R is a polybutenyl group having a molecular weight of 700-5000 and at least one group R" is a polybutenyl group having a molecular weight of 1000-3000.
6. A composition as claimed in any one of claims 1 to 5, wherein the oxyalkylated amine is an oxyalkylated polyalkyleneamine in which the alkyleneamine groups are ethyleneamine groups, propyleneamine groups, or a mixture thereof.
7. A composition as claimed in claim 6, wherein the oxyalkylated polyalkyleneamine is an oxyethylated polyethyleneamine containing one to 6 ethyleneamine units.
8. A composition as claimed in any one of claims 2 to 7, wherein the boronated dispersant has been made by a process comprising reacting in any sequence or altogether.
(a) 1 mole of a polybutenyl succinic anhydride in which the polybutenyl group has a molecular weight of 700-5000,
(b) 0.2 to 2.0 moles of an oxyalkylated palyethleneamine containing 1 to 6 ethyleneamino units, and
(c) 0.001 to 5.0 moles of a boron oxide, a boron acid, an ester of a boron acid, a salt of a boron acid, a boron halide, or a mixture of any two or more thereof.
9. A composition as claimed in claim 8, wherein the polybutenyl group has a molecular weight of 700-2000, the oxyalkylated polyethyleneamine contains an average of 1-4 oxyethylene units per molecule of polyethyleneamine and the polyethyleneamine contains an average of 2-6 ethyleneamino units per molecule.
10. A composition as claimed in claim 8 or claim 9, wherein the boron compound is a boric acid.
11. A composition as claimed in any one of claims 2 to 10, wherein the Mannich dispersant has been made by a process comprising reacting in any sequence or altogether.
(a) one mole of a polybutenyl phenol wherein the polybutenyl group has a molecular weight of 700-7000,
(b) 0.9-2.5 moles of formaldehyde or of a formaldehyde precursor,
(c) 0.1-2.0 moles of an amine containing 1 to 30 carbon atoms and 2 to 10 nitrogen atoms, at least one of which is in a primary amine group,
(d) 0 up to 3 moles of a fatty acid, and
(e) 0 up to 2.0 moles of a boron oxide, a boron acid, an ester of a boron acid, a salt of a boron acid, a boron halide, or a mixture of any two or more thereof.
12. A composition as claimed in claim 11, wherein the amine is N, N-dimethyl-1, 3-propanedianine or a polyethyleneamine containing an average of 1-6 ethyleneamino units.
13. A composition as claimed in claim 11 or claim 12, wherein the fatty acid (d) is oleic acid in an amount of 0.1-2.0 moles per mole of the polybutenyl phenol and the boron compound (e) is boric acid in an amount of 0.01-1.0 moles per mole of the polybutenyl phenol.
14. A composition as claimed in any one of claims 11 to 13, wherein the amine is an oxyethylated polyethyleneamine containing an average of 2-6 ethyleneamino units per molecule and 1-4 oxyethylene units per molecule.
15. A composition as claimed in any one of claims 11 to 14, wherein the polybutenyl group of the polybutenyl phenol has a molecular weight of 1000-3000.
16. An additive package formulated for addition to lubricating oil to obtain a formulated motor oil suitable for use in an internal combustion engine and containing a mixture of the dispersant ingredients of a composition as claimed in any one of the claims 1 to 15.
17. A lubricating oil composition comprising an oil of lubricating viscosity containing a dispersant amount of the dispersant ingredients of a composition as claimed in any one of claims 1 to 15.
18. A method of imparting dispersancy. properties to a lubricating oil which comprises incorporating in the oil the dispersant ingredients of a composition as claimed in any one of claims 1 to 15.
19. A boronated hydrocarbon-substituted succinic amide/imide and/or ester of an oxyalkylated amine or a Mannich condensation product of a hydrocarbon-substituted phenol, formaldehyde and an amine, and, optionally a boronating agent and/or a fatty acid, in either case intended for use in a synergistic dispersant mixture comprising at least one representative of each of the aforesaid dispersants.
EP82301504A 1981-03-23 1982-03-23 Dispersant composition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture Expired EP0061346B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US24628081A 1981-03-23 1981-03-23
US246280 2002-09-18

Publications (3)

Publication Number Publication Date
EP0061346A2 true EP0061346A2 (en) 1982-09-29
EP0061346A3 EP0061346A3 (en) 1983-07-20
EP0061346B1 EP0061346B1 (en) 1985-12-04

Family

ID=22930008

Family Applications (1)

Application Number Title Priority Date Filing Date
EP82301504A Expired EP0061346B1 (en) 1981-03-23 1982-03-23 Dispersant composition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture

Country Status (4)

Country Link
EP (1) EP0061346B1 (en)
JP (1) JPS6024156B2 (en)
CA (1) CA1168649A (en)
DE (1) DE3267749D1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0454380A1 (en) * 1990-04-20 1991-10-30 Ethyl Petroleum Additives, Inc. Lubricating oil composition containing combination of succinimide and mannich base dispersants
EP0499384A1 (en) * 1991-01-31 1992-08-19 Ethyl Corporation Lube oil dispersant borating agent

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1199318A (en) * 1982-03-29 1986-01-14 Amoco Corporation Borated lube oil additive
CA2341924C (en) * 2000-03-28 2011-06-07 Chevron Oronite Company Llc Lubricant composition for air-cooled two-stroke cycle engines
WO2013006303A1 (en) * 2011-07-07 2013-01-10 The Lubrizol Corporation Lubricant providing improved cleanliness for two-stroke cycle engines

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3087936A (en) * 1961-08-18 1963-04-30 Lubrizol Corp Reaction product of an aliphatic olefinpolymer-succinic acid producing compound with an amine and reacting the resulting product with a boron compound
US3373111A (en) * 1963-10-14 1968-03-12 Lubrizol Corp Reaction products of an organic epoxide and an acylated polyamine
US3725277A (en) * 1966-01-26 1973-04-03 Ethyl Corp Lubricant compositions
US3756953A (en) * 1965-10-22 1973-09-04 Standard Oil Co Vatives of high molecular weight mannich reaction condensation concentrate and crankcase oils comprising oil solutions of boron deri
US3803039A (en) * 1970-07-13 1974-04-09 Standard Oil Co Oil solution of aliphatic acid derivatives of high molecular weight mannich condensation product

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3087936A (en) * 1961-08-18 1963-04-30 Lubrizol Corp Reaction product of an aliphatic olefinpolymer-succinic acid producing compound with an amine and reacting the resulting product with a boron compound
US3373111A (en) * 1963-10-14 1968-03-12 Lubrizol Corp Reaction products of an organic epoxide and an acylated polyamine
US3756953A (en) * 1965-10-22 1973-09-04 Standard Oil Co Vatives of high molecular weight mannich reaction condensation concentrate and crankcase oils comprising oil solutions of boron deri
US3725277A (en) * 1966-01-26 1973-04-03 Ethyl Corp Lubricant compositions
US3803039A (en) * 1970-07-13 1974-04-09 Standard Oil Co Oil solution of aliphatic acid derivatives of high molecular weight mannich condensation product

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0454380A1 (en) * 1990-04-20 1991-10-30 Ethyl Petroleum Additives, Inc. Lubricating oil composition containing combination of succinimide and mannich base dispersants
EP0499384A1 (en) * 1991-01-31 1992-08-19 Ethyl Corporation Lube oil dispersant borating agent

Also Published As

Publication number Publication date
JPS57202388A (en) 1982-12-11
CA1168649A (en) 1984-06-05
EP0061346A3 (en) 1983-07-20
EP0061346B1 (en) 1985-12-04
DE3267749D1 (en) 1986-01-16
JPS6024156B2 (en) 1985-06-11

Similar Documents

Publication Publication Date Title
US4426305A (en) Lubricating compositions containing boronated nitrogen-containing dispersants
US4173540A (en) Lubricating oil composition containing a dispersing-varnish inhibiting combination of polyol ester compound and a borated acyl nitrogen compound
CA1090320A (en) Lubricating oil composition containing a dispersing- varnish inhibiting combination of nitrogen-containing additives
KR960014935B1 (en) Amine compatibility aids in lubricating oil composition
EP0020037B1 (en) Oil-soluble friction-reducing additive, process for the preparation thereof, and lubricating oil or fuel composition containing the additive
US4105571A (en) Lubricant composition
CN88103104A (en) Prepare improving one's methods of stable oleaginous composition
JPS6215296A (en) Oil-soluble dispersant useful for oily composition
JPS63170414A (en) Lactone modified, esterfied or aminated additive useful for oily composition and composition containing the same
US3679585A (en) Lubricant compositions
US4293432A (en) Lubricating oil composition
US4401581A (en) Nitrogen-containing ashless dispersants and lubricating oil composition containing same
US4866140A (en) Lactone modified adducts or reactants and oleaginous compositions containing same
JP3806950B2 (en) Lubricating additive composition
CA1180320A (en) Co-dispersant stabilized friction modifier lubricating oil composition
US4927562A (en) Elastomer-compatible oxalic acid acylated alkenylsuccinimides
EP0136185A2 (en) Process for boronating dispersants, boronated dispersants and fluid compositions containing the same
EP0061346B1 (en) Dispersant composition for lubricating oil, additive packages and lubricating oil compositions comprising the dispersant ingredients of said composition, a method of imparting dispersancy to a lubricating oil, and ingredients intended for use in a dispersant mixture
EP0471124B1 (en) Polyether substituted mannich bases as fuel and lubricant ashless dispersants
JP2824062B2 (en) Polyolefin succinimide polyamine alkyl acetoacetate adduct dispersant
JPH01502670A (en) Conjugated polyamine lubricant additives derived from hydrocarbyl polynitriles and polyamines
US4705642A (en) Haze, oxidation, and corrosion resistant diesel engine lubricant
US4374033A (en) Dispersant and lubricating oil containing the dispersant
KR100242407B1 (en) Low molecular weight basic nitrogen-containing reaction products as enhanced phosphorous/boron carriers in lubrication oils
US5068046A (en) Lubricant composition comprising an octadecylene oxide polyamine reaction product

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Designated state(s): BE DE FR GB IT NL

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Designated state(s): BE DE FR GB IT NL

17P Request for examination filed

Effective date: 19830603

ITF It: translation for a ep patent filed
GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Designated state(s): BE DE FR GB IT NL

ET Fr: translation filed
REF Corresponds to:

Ref document number: 3267749

Country of ref document: DE

Date of ref document: 19860116

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
ITTA It: last paid annual fee
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 19930215

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 19930225

Year of fee payment: 12

Ref country code: BE

Payment date: 19930225

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 19930226

Year of fee payment: 12

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 19930331

Year of fee payment: 12

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Effective date: 19940323

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Effective date: 19940331

BERE Be: lapsed

Owner name: EDWIN COOPER INC.

Effective date: 19940331

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Effective date: 19941001

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee
GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 19940323

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Effective date: 19941130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: DE

Effective date: 19941201

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST